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Relative size

The space filling model developed by Corey, Pauling, and Koltun is also known as the CPK model, or scale model [197], It shows the relative volume (size) of different elements or of different parts of a molecule (Figure 2-123d). The model is based on spheres that represent the "electron cloud . These atomic spheres can be determined from the van der Waals radii (see Section 2.10.1), which indicate the most stable distance between two atoms (non-bonded nuclei). Since the spheres are all drawn to the same scale, the relative size of the overlapping electron clouds of the atoms becomes evident. The connectivities between atoms, the bonds, are not visualized because they are located beneath the atom spheres and are not visible in a non-transparent display (see Section 2.10). In contrast to other models, the CPK model makes it possible to visualize a first impression of the extent of a molecule. [Pg.133]

HyperClicm cati plot orbital wave fuuctious resulting fmni serni-cmpirical and ah i/iitw quan tii m m ecli an ica I calculations. It is ill tercstiu g to view both tli c u tidal properties an d th e relative sizes of the wave functions. Orbital wave functiou s can provide dietni-cal in sigh is. [Pg.9]

The relative sizes ofthe poten tial barriers in dicate that the AF force con Stan t is larger th an the V con stan t. fh e ph ase sh ift is 180 degrees for th e Fourier compoiien t with a two-fold barrier. Minima occur at 180, 0, and I 80 degrees and maxima at 90 and 90... [Pg.25]

HyperChem can plot orbital wave functions resulting from semi-empirical and ab initio quantum mechanical calculations. It is interesting to view both the nodal properties and the relative sizes of the wave functions. Orbital wave functions can provide chemical insights. [Pg.9]

Figure 6.10 Schematic representation of the distribution of surfactant in an emulsion polymerization. Note the relative sizes of suspended particles. [From J. W. Vanderhoff, E. B. Bradford, H. L. Tarkowski, J. B. Shaffer, and R. M. Wiley,Chem. 34 32(1962).]... Figure 6.10 Schematic representation of the distribution of surfactant in an emulsion polymerization. Note the relative sizes of suspended particles. [From J. W. Vanderhoff, E. B. Bradford, H. L. Tarkowski, J. B. Shaffer, and R. M. Wiley,Chem. 34 32(1962).]...
A dsc scan of a typical commercial ionomer shows two endotherms at about 50 and 98°C, respectively. The size of the lower peak can be correlated with stiffness and yield point. The thermal history of the sample influences the relative size of the lower peak and moves it to higher temperatures, while the upper peak decreases in size but remains at the same temperature. Room temperature aging also increases the size of the lower endotherm. [Pg.407]

Fig. 1. Schematic of the cross section of a mammal s skin. The relative size and function of the parts depend on the species and breed of the animal. For goats, where the wool or hair is sparse because it is not needed for warmth, the skin is dense to provide protection for sheep protected primarily by heavy wool, the skin contains more oil (sebaceous) glands to lubricate the wool for catde, both the hair and the heavy hide stmcture protect the animal (3). Fig. 1. Schematic of the cross section of a mammal s skin. The relative size and function of the parts depend on the species and breed of the animal. For goats, where the wool or hair is sparse because it is not needed for warmth, the skin is dense to provide protection for sheep protected primarily by heavy wool, the skin contains more oil (sebaceous) glands to lubricate the wool for catde, both the hair and the heavy hide stmcture protect the animal (3).
Fig. 25. Reverse osmosis, ultrafiltration, microfiltration, and conventional filtration are related processes differing principally in the average pore diameter of the membrane filter. Reverse osmosis membranes are so dense that discrete pores do not exist transport occurs via statistically distributed free volume areas. The relative size of different solutes removed by each class of membrane is illustrated in this schematic. Fig. 25. Reverse osmosis, ultrafiltration, microfiltration, and conventional filtration are related processes differing principally in the average pore diameter of the membrane filter. Reverse osmosis membranes are so dense that discrete pores do not exist transport occurs via statistically distributed free volume areas. The relative size of different solutes removed by each class of membrane is illustrated in this schematic.
Ideally, the chance of a spherical particle having diameter t passing through an opening would be zero for all particles of relative size djb > 1 and one for all particles of relative size djb < 1. A plot of the probabiUty-of-passing vs size (Fig. 1, curve D) is a step function, and the separation size, so-called cut size, is d/b = 1. A perfect separation is one where all particles of size less than the cut size pass and all particles of size greater than the cut size are retained. [Pg.433]

In thermoelectric cooling appHcations, extensive use has been made of cascaded systems to attain very low temperatures, but because the final stage is so small compared to the others, the thermal flux is limited (Eig. 3). The relative sizes of the stages ate adjusted to obtain the maximum AT. Thus, for higher cooling capacity, the size of each stage is increased while the area ratios ate maintained. [Pg.505]

Fig. 3. Three-Stage cascaded thermopile. The relative sizes of the stages must be adjusted to obtain the maximum AT. Fig. 3. Three-Stage cascaded thermopile. The relative sizes of the stages must be adjusted to obtain the maximum AT.
The development of a continuous grinding index was the focus of work in the late 1970s (59). The laboratory test equipment used is similar to that for the Hardgrove test but permits classifying the product and recycling the oversize material. An improved correlation is obtained that may, however, need to be corrected for the relative sizes of the test grinding balls versus those used in commercial-scale equipment. The continuous grinding index is especially useful for lower rank coals. [Pg.222]

T1) Relative size distribution Fract3ire stress under three-point bend loading kg/cm psf... [Pg.1821]

The relative size of hazard zones from possible loss of containment and releases to the atmosphere is much smaller for the cases in which the material is diluted, compared to the anhydrous materials. This is illustrated in Fig. 26-28 for monomethylamine. [Pg.2307]

FIG. 27-45 Location and relative size of each of four passes of the flue gas through a fire-tube boiler. From Cleaver Brooks, Inc. Reproduced from Gas Engineer s Handbook, Industrial Press, New York, 1965, with permission. )... [Pg.2398]

In the ceramics field many of the new advanced ceramic oxides have a specially prepared mixture of cations which determines the crystal structure, through the relative sizes of the cations and oxygen ions, and the physical properties through the choice of cations and tlreh oxidation states. These include, for example, solid electrolytes and electrodes for sensors and fuel cells, fenites and garnets for magnetic systems, zirconates and titanates for piezoelectric materials, as well as ceramic superconductors and a number of other substances... [Pg.234]

What if the above relationship between the resonant induetor and eapaeitor were pushed one direetion or the other. One eould use a large L and a small C or viee versa. The relative size of the two eomponents does affeet some behaviors of the eireuit. For instanee, if a small C is used in a ZVS OR... [Pg.159]

It is interesting to note that although the market for natural rubber has grown considerably, that for the other diene rubbers has either been of slow growth or has declined. Data for approximate overall plastics production (not from IlSRP data) have also been included as a comparison of the relative sizes of the rubber and plastics markets. [Pg.281]

The forces applied by an impeller to the material contained in a vessel produce characteristic flow patterns that depend on the Impeller geometry, properties of the fluid, and the relative sizes and proportions of the tank, baffles and impeller. There are three principal types of flow patterns tangential, radial and axial. Tangential flow is observed when the liquid flows parallel to the path described by the mixer as illustrated in Figure 7. [Pg.446]

Tables 13-2 and 13-3 elueidate how the eommon dimensionless groups are derived. The boundary eonditions governing the differential equations eombined with the relative size of the system should be eonsidered when determining dimensionless parameters. Using Table 13-2 to determine the dimensionless groups for any of the three equations, divide one set of the dimensions into all the others ineluding the boundary eonditions. Tables 13-2 and 13-3 elueidate how the eommon dimensionless groups are derived. The boundary eonditions governing the differential equations eombined with the relative size of the system should be eonsidered when determining dimensionless parameters. Using Table 13-2 to determine the dimensionless groups for any of the three equations, divide one set of the dimensions into all the others ineluding the boundary eonditions.
The air is then discharged through the rear plenum into the space benvcen the supply and exhaust filters hicated at the top of the cabinet. Due to the relative size of these two filters, approximately 30% of the air passes through the exhaust HEPA filter and 70% recirculates through the supply HEPA filter back into the work zone. Most Class IIA cabinets have dampers to modulate this 30%/70% division of airflow. [Pg.987]

The resolution required in any analytical SEC procedure, e.g., to detect sample impurities, is primarily based on the nature of the sample components with respect to their shape, the relative size differences of species contained in the sample, and the minimal size difference to be resolved. These sample attributes, in addition to the range of sizes to be examined, determine the required selectivity. Earlier work has shown that the limit of resolvability in SEC of molecules [i.e., the ability to completely resolve solutes of different sizes as a function of (1) plate number, (2) different solute shapes, and (3) media pore volumes] ranges from close to 20% for the molecular mass difference required to resolve spherical solutes down to near a 10% difference in molecular mass required for the separation of rod-shaped molecules (Hagel, 1993). To approach these limits, a SEC medium and a system with appropriate selectivity and efficiency must be employed. [Pg.30]

Caution The order of elution of solutes smaller than a tetrapeptide may be in order of decreasing polarity rather than decreasing molecular weight. This reflects the relative size of their spheres of hydration. [Pg.260]

Note also that the relative sizes cf the altered zones are not to scale (e.g., choosing a higher value for the level of concern does not always result in a smaller zone than the use of greater wind speed and less atmospheric stability). [Pg.505]


See other pages where Relative size is mentioned: [Pg.366]    [Pg.420]    [Pg.444]    [Pg.123]    [Pg.67]    [Pg.337]    [Pg.411]    [Pg.200]    [Pg.322]    [Pg.254]    [Pg.354]    [Pg.293]    [Pg.232]    [Pg.248]    [Pg.351]    [Pg.1656]    [Pg.1656]    [Pg.65]    [Pg.289]    [Pg.354]    [Pg.36]    [Pg.2]    [Pg.4]    [Pg.409]    [Pg.784]    [Pg.260]   
See also in sourсe #XX -- [ Pg.25 ]

See also in sourсe #XX -- [ Pg.216 , Pg.470 , Pg.471 ]




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